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rauchgasnassentschwefelungsvorrichtung and procedures for rauchgasnassentschwefelung

机译:烟气湿法脱硫装置及烟气湿法脱硫程序

摘要

Exhaust (Flue) gas of boiler is introduced through gas inlet part (port) (2) of flue-gas desulfurization apparatus (system), and absorbent liquid sprayed from spray nozzle (5) of absorbent liquid spray section (4) is trapped (stored) in liquid trapping (recirculation tank) section (7). There, agitation is performed by means of propeller (11) of oxidation agitator (8) to thereby oxidize SO 2 absorbed from the exhaust (flue) gas into gypsum. In the liquid trapping section (7), oxidation air is fed from posterior air pipe (10) and anterior air pipe (13) behind and ahead of liquid propulsion (to the rear and front of a liquid discharge) by the propeller (11). Thus, even when the amount of oxidation air must be increased in accordance with an increase of boiler load, the oxidation efficiency can be enhanced without increasing of the number of agitators. Accordingly, there can be provided a wet flue-gas desulfurization apparatus (system) and method with which even when the amount of oxidation air fed to the liquid trapping section is increased, highly efficient oxidation can be performed without increasing the number of agitators installed and the operating cost.
机译:锅炉的废气从烟气脱硫装置(系统)的进​​气口(端口)(2)导入,从吸收液喷雾部(4)的喷嘴(5)喷出的吸收液被捕集(储存)在液体收集(再循环槽)部分(7)中。在那里,借助于氧化搅拌器(8)的螺旋桨(11)进行搅拌,从而将从废气(烟道气)吸收的SO 2氧化为石膏。在液体捕集部(7)中,通过螺旋桨(11)从液体推进前后的后空气管道(10)和前空气管道(13)供给氧化空气(排液的前后)。 。因此,即使当必须根据锅炉负荷的增加而增加氧化空气的量时,也可以在不增加搅拌器数量的情况下提高氧化效率。因此,可以提供一种湿式烟道气脱硫装置(系统)和方法,利用该湿式烟气脱硫装置和方法即使增加了供给至液体捕集部的氧化空气的量,也可以进行高效的氧化,而无需增加所安装的搅拌器的数量。运营成本。

著录项

  • 公开/公告号DE602006021341D1

    专利类型

  • 公开/公告日2011-05-26

    原文格式PDF

  • 申请/专利权人 BABCOCK-HITACHI K.K.;

    申请/专利号DE20066021341T

  • 申请日2006-09-20

  • 分类号B01D53/50;B01D53/18;B01D53/77;

  • 国家 DE

  • 入库时间 2022-08-21 17:46:27

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